02466nam a2200241 a 4500 vtls000075161 KUKTEM 20251114204551.0 131008t2012 my a f m 000 0 eng d THE0004204(Local) 201905152025 farhana 201311181658 nabilah 201310231033 nabilah 201310081449 nabilah UMP TP157 .N58 2012 rs Bc. Ngu, Ming Tiong Development of an extractive reactor block in the aspen plus simulator / Ngu Ming Tiong Kuantan, Pahang : UMP, 2012 xiv, 30 p. : ill. ; 30 cm. + 1 CD-ROM Project paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang – 2012 Bibliography : p. 25-26 The design and operation issues for extractive reactor system are considerably more complex than those involved for either conventional extraction column or convention reactors. The introduction of an in situ separation function within the reaction zone leads to complex interactions between liquid-liquid equilibrium, liquid-liquid mass transfer, intra-catalyst diffusion (for homogeneously catalysed processes) and chemical kinetics. The advantages of such alternatives is the use of simultaneous extraction and reaction to improve the yields and/or selectivity to the products, and also that they require smaller recycle flows. This research is to purpose a suitable configuration for extractive reaction by identify the important parameter that affect the process and develop the kinetic subroutine in Aspen Plus simulation. The reactor block is design by using the Aspen plus simulation to set up and specifies the application type. It is combining with an Excel spreadsheet to performance the calculations by using Dynamic Data Exchange (DDE). From the simulation, it show out that the production of for the first stream with 249.430 kmol/hr methanol, 687.099 kmol/hr fatty acid methyl ester, and 336.185 kmol/hr glycerol. However, for the second stream which produce 133.780 kmol/hr triglyceride, 137.452 kmol/hr methanol and 118.889 kmol/hr fatty acid methyl ester. For the reactor block design it is an integrate current, future technology in exciting plant and also perform plant optimization and control to improve the plant competitiveness. Chemical reactors 0 0 0 1 10000 10000 2019-09-04 0 TP157 .N58 2012 rs Bc. 0000074905 2019-09-04 00:00:00 1 2019-09-04 PSM 0 0 0 1 10000 10000 2019-09-04 0 CD 7152 | TP157 .N58 2012 rs Bc. 0000074906 2019-09-04 00:00:00 1 2019-09-04 PSM VIRTUA40 4233 4239 VTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5020*5040*5200*6500*9992